Jose Campos-Martin

Dr. Jose Campos-Martin

Instituto de Catálisis y Petroleoquímica, CSIC
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Research Focus & Metrics

Academic Career Length

32Years (1995-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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23 October 2006 in Angewandte Chemie International Edition
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Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
GBGema Blanco‐Brieva
Gema Blanco‐Brieva
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro

9 March 2010 in Journal of Chemical Technology & Biotechnology
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Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
MSMaria del Carmen Capel Sánchez
Maria del Carmen Capel Sánchez
PPP. Perez‐Presas
P. Perez‐Presas
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro

4 February 2011 in Catalysis Science & Technology
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BPBarbara Pawelec
Barbara Pawelec
Rufino Manuel NavarroRufino Manuel Navarro
Rufino Manuel Navarro
Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro
We, the named authors, hereby wholly retract this Catalysis Science & Technology article, due to significant similarity with previously published work. Signed: B. Pawelec, R. M. Navarro, J. M. Campos-Martin and J. L. G. Fierro, October 2012. Retraction endorsed by Jamie Humphrey, Editor, Catalysis Science & Technology.

11 October 2004 in Green Chemistry
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Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
MSMaria del Carmen Capel Sánchez
Maria del Carmen Capel Sánchez
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro
This paper describes the oxidation of several model S-containing molecules with hydrogen peroxide in a two liquid–liquid (L–L) phase system with a phase transfer catalyst under atmospheric pressure in the 333–353 K temperature range. The influence of the reaction temperature, the nature of the substrate, the solvent, the molar ratio of the oxidant (H2O2) and the S-containing molecule were examined. The reaction rates of the oxidative desulfurization (ODS) reaction were found to increase with the temperature, and with the molar ratio of H2O2 and the S-containing molecule. The potential of this methodology is illustrated by the complete S-removal from a 5.0 wt% dibenzothiophene mixture at 353 K, under excess of H2O2 oxidant in less than three hours of reaction. In addition, the ODS reaction was strongly enhanced when the water solvent was replaced by acetonitrile. The very high ODS reaction rate observed with the acetonitrile solvent could be explained in terms of the much higher solubility of the sulfone reaction product in this solvent and also by its very low surface tension, which facilitates the transfer of products and reagents at the polar–apolar interface. Finally, the very mild sulfoxidation reaction was applied to a kerosene fraction. The results revealed that S-levels below 25 ppm are achieved at 353 K upon using a H2O2 ∶ substrate molar ratio of 2.5 ∶ 1.

1 January 2011 in Fuel
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Journal Article
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GBG. Blanco-Brieva
G. Blanco-Brieva
Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
SASaeed Al-Zahrani
Saeed Al-Zahrani
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro

28 June 2004 in Green Chemistry
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ACA. Campanella
A. Campanella
MBM. A. Baltanás
M. A. Baltanás
MSMaria del Carmen Capel Sánchez
Maria del Carmen Capel Sánchez
Jose Campos-MartinJose Campos-Martin
Jose Campos-Martin
Jose L.G. FierroJose L.G. Fierro
Jose L.G. Fierro
We report a study of the epoxidation of soybean oil and soybean methyl esters with hydrogen peroxide in dilute solution (6 wt%) using an amorphous heterogeneous Ti/SiO2 catalyst in the presence of tert-butyl alcohol. The influence of some relevant process variables such as temperature and the hydrogen peroxide-to-double bond molar ratio on performance is examined. The highest yields of epoxidized olefins were obtained upon using a H2O2 ∶ substrate molar ratio of 1.1 ∶ 1. Higher ratios than this were not effective for speeding up the reaction. Under the experimental conditions employed in this work, no degradation of the oxirane ring was observed.